Layered platinum on freestanding palladium nano-substrates for electrocatalytic applications and methods of making thereof

ABSTRACT

Core-shell nanostructures with platinum overlayers conformally coating palladium nano-substrate cores and facile solution-based methods for the preparation of such core-shell nanostructures are described herein. The obtained Pd@Pt core-shell nanocatalysts showed enhanced specific and mass activities towards oxygen reduction, compared to a commercial Pt/C catalyst.

CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a divisional application that claims the benefit ofand priority to co-pending U.S. Nonprovisional patent application Ser.No. 14/659,879, filed on Mar. 17, 2015, the contents of which areincorporated by reference herein in its entirety.

STATEMENT REGARDING FEDERALLY SPONSORED RESEARCH OR DEVELOPMENT

This invention was made with government support under Grant No.DMR1215034 awarded by the National Science Foundation. The governmenthas certain rights in the invention.

FIELD OF THE INVENTION

The present invention generally relates to layered platinum onfreestanding palladium nano-substrates, methods of making suchnanostructures, and catalytic uses thereof.

BACKGROUND OF THE INVENTION

Because platinum is one of the scarcest noble metals on the planet, theavailability of platinum has become a major concern for existing andemerging applications using platinum catalysts. For example, platinumcatalysts are typically the most common catalysts used in the oxygenreduction reaction (ORR), which occurs on the cathode of aproton-exchange membrane fuel cell (PEMFC); see Steele, B. et al. Nature2001, 414, 345-332 and Debe, M. K. Nature 2012, 486, 43-51.

Various studies have been carried out to increase the utilizationefficiency of platinum and concurrently reduce the content of platinumin a catalyst. Methods are being developed to improve the activities ofplatinum-based catalysts. One of the most promising approaches has beento deposit platinum atoms as ultrathin skins of only a few atomic layersonto nanoparticles made of more abundant and/or less expensive metal ormetal alloys; see Sasaki, K. et al. Nat. Commun, 2012, doi:10.1038/ncomms2124 and Zhang, J. et al. Angew. Chem. Int. Ed. 2005, 44,2132-2135. Such deposition of only a few atomic layers of platinum onthe surface of facet-controlled nanocrystals made of another metal, suchas palladium, provides an attractive strategy for maximizing theactivity in terms of the platinum mass loading.

For single-crystal substrates, it has been shown that ultrathin coatingsof platinum with well-controlled thicknesses can be achieved via vacuumdeposition, followed by annealing at a very high temperature (≥1000°C.); see Toyoda, E. et al. Angew. Chem., Int. Ed. 2013, 52, 4137-4140.Nevertheless, a limitation of this technique is that it cannot beextended to substrates having nanometer sizes or to form coatings onsubstrates in solution phase.

U.S. Pat. No. 7,691,780 to Adzic et al. describes palladium or palladiumalloy particles coated with platinum layer(s) which wereelectrodeposited via a method which involves first underpotentiallydepositing (UPD) copper monolayers or sub-monolayers on palladium orpalladium alloy particles and then contacting the copper-coatedparticles with a platinum salt to cause spontaneous redox displacementof the copper atomic layer to firm a platinum layer. These platinumcoated palladium or palladium-alloy particles were shown to possessenhanced mass activity toward ORR. Adzic and co-workers workers (Zhang,J. et al. J. Phys. Chem. B 2004, 108, 10955-10964) reported thatplatinum monolayers deposited by such displacement of a copper atomiclayer by a platinum consisted of interconnected islands on the surfaceof the palladium particles with increased atomic scale roughness. Theplatinum-coated palladium particles described by Adzic et al. thereforewere shown to suffer from surface coverage issues. The method ofdeposition described is based on electrochemical approach, which couldlimit the scalability for producing such particles.

While prior studies have demonstrated the feasibility of generatingPd@Pt core-shell nanocrystals having ultrathin skins of platinum, it hasbeen extremely difficult (or even impossible) to precisely and reliablycontrol the thicknesses of the platinum overlayers down to the atomicscale. For example, traditional atomic layer deposition (ALD) in a gasphase and most of the solution-phase methods reported thus far oftengenerate platinum overlayers with a polycrystalline structure and uneventhickness; see Aaltonen, T. et al. Chem. Mater. 2003, 15, 1924-1928 andMackus, A. J. M. et al. Chem. Mater. 2013, 25, 1905-1911. Owing to theintrinsic high surface free energy and interatomic bond energy (307kJ/mol) of platinum, direct deposition of platinum tends to favor anisland growth mode (Volmer-Weber mode) see Fan, F.-R. et al. J. Am.Chem. Soc. 2008, 130, 6949-6951 and Peng, Z. et al. Nano Today 2009, 4,143-164. Methods developed to-date have been based on solution phasesynthetic conditions which are too mild to provide sufficientthermodynamic energy to break down the limitation of the strongplatinum-platinum interaction. As a result, the newly formed reducedplatinum atoms preferentially self-nucleate, rather than tile on thesurface of palladium nano-substrates (seeds).

Challenges and difficulties remain in the synthesis of core-shellnanostructures formed by deposition of layers of platinum on the surfaceof the nanoscale palladium substrates having precise control at theatomic scale. Development of such core-shell nanostructures can lead toefficient ORR catalysts which can dramatically increase the efficiencyof fuel cells.

Thus, there exists a need for platinum on palladium core-shellnanostructures having platinum overlayers with precisely and reliablycontrolled thicknesses, as well as development of novel methods ofproducing such core-shell nanostructures. There is also a need for suchplatinum on palladium core-shell nanostructures for use as catalysts foroxygen reduction reaction (ORR).

Therefore, it is an object of the invention to provide platinum andpalladium core-shell nanostructures having conformal platinum overlayerson a palladium core.

It is a further object of the invention to provide facile and scalablesolution-based reaction methods and conditions for synthesizing suchcore-shell nanostructures.

It is another object of the invention is to use the core-shell nanodeveloped as catalytic materials.

It is another object of the invention to use the core-shellnanostructures as oxygen reduction reaction (ORR) catalysts thatcatalyze oxygen reduction at fuel cell cathodes.

SUMMARY OF THE INVENTION

The present disclosure relates to various embodiments of core-shellnanostructures having platinum overlayers on a nano-substrate coreformed of palladium, methods for the preparation of such core-shellnanostructures, and their use in electrocatalytic applications asdescribed herein.

One embodiment is a method wherein palladium nano-substrates act asseeds onto which one or more epitaxially deposited overlayers ofzero-valent platinum are formed to produce platinum on palladiumnanostructures, denoted Pd@Pt_(nL), wherein the value of “n” denotes thenumber of platinum overlayers and “L” is an abbreviation of the termlayer(s).

The method includes forming core-shell nanostructures having a palladiumnano-substrate core and epitaxially depositing one or more conformaloverlayers of zero-valent platinum atoms by addition of a solutioncontaining a platinum-containing compound to a solution containing aplurality of the palladium nano-substrates and a reducing agent andheating the mixture to a temperature in the range of about 75 to about250° C. to induce epitaxial layer-by-layer deposition of one or moreplatinum overlayers onto the palladium nano-substrates.

Conformal deposition of reduced platinum atoms to form one or moreoverlayers on the palladium nano-substrates, in general, occurs via aninitial deposition of the platinum atoms at corners of thenano-substrates. The surface hound platinum atoms then diffuse away fromthe corners to the edges and side faces of the palladiumnano-substrates. As a result, the morphology of the final core-shellnanostructures is largely determined by the difference in ratesresponsible for platinum atom deposition (V_(deposition)) and surfacediffusion (V_(diffusion)); see FIG. 1 . The V_(deposition) andV_(diffusion) rates can be controlled according to the reactionconditions applied during the method as described further below.

Another embodiment provides a method in which the deposition of the oneor more zero-valent platinum overlayers onto the palladiumnano-substrates is carried out in a polyol-type solvent, such asethylene glycol (EG), and the reaction solution is preferably heated toa temperature in the range of about 150 to about 250° C. According toyet another embodiment of the method, the deposition of the one or morezero-valent platinum overlayers onto the palladium nano-substrates canbe carried out in a water-based solvent, such as deionized water, andthe reaction solution is preferably heated to a temperature in the rangeof about 85 to about 100° C.

Another embodiment provides a method in which palladium nano-substrates(seeds) onto which epitaxial layer-by-layer deposition of zero-valentplatinum overlayers is applied have a shape chosen from the groupconsisting of cubic, concave cubic, tetrahedral, bipyramidal,octahedral, icosahedral, and decahedral shapes. In certain embodimentsthe aforementioned nano-substrate shapes can be non-truncated (perfect)or they can be truncated, having various degrees of truncation at thecorners and/or edges. In certain other embodiments, the nano-substratesseeds can be rod (i.e., rectangular, pentagonal, octagonal), bar (i.e.,rectangular), wire (i.e., rectangular, octagonal, pentagonal), and plateshaped. The selection of shape and/or degree of truncation can becontrolled according to the reaction conditions used.

The Pd@Pt_(nL) core-shell nanostructures synthesized according to themethods described herein possess a palladium nano-substrate coreconformally coated with one or more atomic overlayers of epitaxiallydeposited zero-valent platinum atoms. The Pd@Pt_(nL) core-shellnanostructures formed typically adopt the shape of the palladiumnano-substrates (seeds) on to which the one or more zero-valentoverlayers were deposited onto. In preferred embodiments, the Pd@Pt_(nL)core-shell nanostructures have about one to about ten atomic overlayersof zero-valent platinum deposited onto them typically via epitaxiallayer-by-layer growth. The one or more zero-valent platinum overlayersformed are uniformly deposited and can form smooth surfaces on thecoated palladium nano-substrates (seeds). The Pd@Pt_(nL) core-shellnanostructures can have an average particle size in the range of aboutone to about 1000 nm, more preferably about one to about 100 nm.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 shows a schematic illustration of the deposition of platinum (Pt)atoms on a palladium (Pd) substrate divided into two major steps: (1)deposition of Pt atoms at the corner sites and (2) surface diffusion ofthe deposited Pt atoms from the corners to the side faces. WhenV_(deposition)<V_(diffusion) as shown in (i), the Pt atoms can evenlyspread on the entire Pd{100} faces, generating Pd@Pt_(nL) core-shellnanostructures with a well-controlled number of Pt atomic layers. WhenV_(deposition)>V_(diffusion), as shown in (ii), the majority of thedeposited Pt atoms have a tendency to remain at the corner sites.

FIG. 2 shows a schematic diagram of the syntheses of Pd@Pt_(nL)octahedra via two different routes involving polyol and water,respectively. For the synthesis in a polyol-based solvent (such asethylene glycol (EG)), a solution of PtCl₆ ²⁻ is added dropwise into thereaction solution containing L-ascorbic acid (AA) at 200° C. Due to theuse of a relatively high temperature, the core-shell octahedra producedhave slight/minor truncation at the corners, just like the starting Pdnano-substrates (seeds). For the synthesis in a water-based solvent, anaqueous solution of PtCl₄ ²⁻ is added in one shot into the reactionsolution containing citric acid (CA) at 95° C. The use of a considerablylower reaction temperature results in the formation of core-shelloctahedra with sharper corners.

FIG. 3A-L shows TEM images and EDX line scans of Pd@Pt_(nL) (n=1, 4, 6)nanocubes. FIGS. 3A-C show low-magnification HAADF-STEM images ofPd@Pt_(6L), Pd@Pt_(4L), and Pd@Pt_(1L) nanocubes, respectively; FIGS.3D-F shows HAADF-STEM images of an individual Pd@Pt_(6L), Pd@Pt_(4L),and Pd@Pt_(1L) nanocube, respectively; FIGS. 3G-I showsatomic-resolution HAADF-STEM images taken from the Pd@Pt_(6L),Pd@Pt_(4L), and Pd@Pt_(1L) nanocube, respectively, revealing the numbersof platinum atomic layers; FIGS. 3J-L shows the EDX line scan profilesof Pd and Pt for the Pd@Pt_(6L), Pd@Pt_(4L), and Pd@Pt_(1L) nanocubealong the white arrows marked on FIGS. 3G, 3H, and 3I.

FIGS. 4A-C shows TEM images of Pd@Pt_(nL) octahedra synthesized usingthe polyol-based protocol. FIGS. 4A, 4B, and 4C show Pd@Pt_(2-3L),Pd@Pt_(3-4L), and Pd@Pt_(4-5L) octahedra as well as the platinum content(wt %) from ICP-MS analysis.

FIGS. 5A-F shows HAADF-STEM images of the Pd@Pt_(2-3L) octahedrasynthesized according to the polyol-based protocol and the EDX line scananalysis of the octahedra; in FIGS. 6A-E, the dark and light regions inthe TEM images correspond to palladium and platinum, respectively. FIG.5F shows the EDX line scan profiles of Pd and Pt for the Pd@Pt_(2-3L)octahedron along the white arrow marked in FIG. 5E.

FIGS. 6A-F shows HAADF-STEM images of the Pd@Pt_(2-3L) octahedrasynthesized according to the water-based protocol and the EDX line scananalysis of the octahedra; in FIGS. 6A-E, the dark and light regions inthe TEM images correspond to palladium and platinum, respectively. FIG.6F shows the EDX line scan profiles of Pd and Pt for the Pd@Pt_(2-3L)octahedron along the white arrow marked in FIG. 6E.

FIGS. 7A-H shows TEM and HAADF-STEM images of Pd@Pt_(2.7L) icosahedra,FIGS. 7A and 7B show TEM images of the Pd@Pt_(2.7L) icosahedra. FIG. 7Cshows an HAADF-STEM image taken from a single Pd@Pt_(2.7L) icosahedraparticle along a 2-fold symmetry axis shows three atomic layers of Pt inthe shell (with a brighter contrast) and Pd atoms in the core; in FIG.7D an HAADF-STEM image of two Pd@Pt_(2.7L) icosahedra and thecorresponding EDX mapping of Pd and Pt is shown confirming a Pd@Ptcore-shell structure. FIGS. 7E and 7F show HAADF-STEM images taken fromthe edges marked by boxes E and F in FIG. 7C, showing the detailedarrangement of the Pd (labeled 1-14) and Pt (labeled 1-15) atoms. FIGS.7G and 7H are duplicates of what are shown in FIGS. 7E and F,respectively, demonstrating, the formation of a corrugated structure forthe Pt overlayers.

FIG. 8 shows a bar graph of the specific ECSAs for the Pd@Pt_(nL)/C(n=1, 2-3, 4, and 6) nanocubes, platinum nanocubes, and commercial Pt/Ccatalysts as measured from the charges associated with H_(upd)desorption between 0.08 and 0.45 V (vs. RHE).

FIG. 9 shows the positive-going ORR polarization curves for thePd@Pt_(nL)/C (n=1, 2-3, 4, and 6) nanocubes, platinum nanocubes, andcommercial Pt/C catalysts at room temperature in O₂-saturated 0.1 Maqueous HClO₄ solutions.

FIGS. 10A-B shows bar graphs of the specific and mass ORR activitiesgiven as kinetic current densities (j_(k)) normalized to the ECSA andplatinum loading of the Pd@Pt_(nL)/C (n=1, 2-3, 4, and 6) nanocubes,platinum nanocubes, and commercial Pt/C catalyst at 0.9 V (vs. RHE),respectively.

FIGS. 11A-B shows bar graphs of the specific ECS As and mass activities,given as the kinetic current densities (j_(k)) at 0.9 V (vs. RHE), ofthe Pd@Pt_(nL)/C (n=1, 2-3, 4, and 6) nanocubes and commercial Pt/C ORRcatalysts before and after 5.000 and 10,000 cycles of accelerateddurability tests.

FIG. 12 shows a bar graph of the specific ECSAs for the Pd@Pt_(nL)/C(n=2-3, 3-4, and 4-5) octahedra, formed by polyol-based synthesis, andcommercial Pt/C catalysts as measured from the charges associated withH_(upd) desorption between 0.08 and 0.4 V (vs. RHE).

FIG. 13 shows the positive-going ORR polarization curves for thePd@Pt_(nL)/C (n=2-3, 3-4, and 4-5) octahedra and commercial Pt/Ccatalysts at room temperature in O₂-saturated 0.1 M aqueous HClO₄solutions.

FIGS. 14A-B shows bar graphs of the specific and mass ORR activitiesgiven as kinetic current densities (j_(k)) normalized to the ECSA andplatinum loading of the Pd@Pt_(nL)/C (n=2-3, 3-4, and 4-5) octahedra andcommercial Pt/C catalyst at 0.9 V (vs. RHE), respectively. In FIG. 14B,the mass activities are given normalized against the masses of Pt andcombined Pd+Pt, respectively.

FIGS. 15A-B shows bar graphs of the specific ECSAs and mass activities,given as the kinetic current densities (j_(k)) at 0.9 V (vs. RHE), ofthe Pd@Pt_(nL)/C (n=2-3, 3-4, and 4-5) octahedra and commercial Pt/C ORRcatalysts before and after 5,000 and 10,000 cycles of accelerateddurability tests.

FIG. 16 shows a bar graph of the specific ECSAs for Pd@Pt_(2-3L)/Coctahedra, formed by water-based synthesis, and commercial Pt/Ccatalysts as measured from the charges associated with H_(upd)desorption between 0.08 and 0.4 V (vs. RHE).

FIG. 17 shows the positive-going ORR polarization curves for thePd@Pt_(2-3L)/C octahedra and commercial Pt/C catalysts at roomtemperature in O₂-saturated 0.1 M aqueous HClO₄ solutions.

FIGS. 18A-B shows bar graphs of the specific and mass ORR activitiesgiven as kinetic current densities (j_(k)) normalized to the ECSAs andplatinum loading of the Pd@Pt_(2-3L)/C octahedra and commercial Pt/Ccatalyst at 0.9 V (vs. RHE), respectively. In FIG. 18B, the massactivities are given normalized against the masses of Pt and combinedPd+Pt, respectively.

FIGS. 19A-B shows bar graphs of the specific ECSAs and mass activities,given as the kinetic current densities (j_(k)) at 0.9 V (vs. RHE), ofthe Pd@Pt_(2-3L)/C octahedra and commercial Pt/C ORR catalysts beforeand after 5,000, 10,000 and 20,000 cycles of accelerated durabilitytests.

FIG. 20 shows a bar graph of the specific ECSAs for the Pd@Pt_(2.7L)/Cicosahedra and commercial Pt/C catalysts as measured from the chargesassociated with H_(upd) desorption between 0.08 and 0.45 V (vs. RHE).

FIG. 21 shows the positive-going ORR polarization curves for thePd@Pt_(nL)/C (n=0.7, 2, 2.7, 43) icosahedra and commercial Pt/Ccatalysts at room temperature in O₂-saturated 0.1 M aqueous HClO₄solutions.

FIGS. 22A-B shows bar graphs of the specific and mass ORR activitiesgiven as kinetic current densities (j_(k)) normalized to the ECSAs andplatinum loading of the Pd@Pt_(nL)/C (n=0.7, 2, 2.7, 4.3) icosahedra andcommercial Pt/C catalyst at 0.9V (vs. RHE), respectively.

FIGS. 23A-B shows HAADF-STEM images of an individual Pd@Pt_(2.7L)icosahedron along a 2-fold symmetry axis after annealing in the electronmicroscope at 300° C. for 30 min. FIG. 23B shows an HAADF-STEM imagetaken from the edge marked by a box in FIG. 23A showing that thecorrugated structure of the platinum shell was retained even afterheating at 300° C. for 30 min and showing the detailed arrangement ofthe Pd (labeled 1-11) and Pt (labeled 1-12) atoms.

FIGS. 24A-B shows bar graphs of the specific ECSAs and mass activities,given as the kinetic current densities (j_(k)) at 0.9 V (vs. RHE), ofthe Pd@Pt_(2.7L)/C octahedra and commercial Pt/C ORR catalysts beforeand after 5,000 and 10,000 cycles during accelerated durability tests.

DETAILED DESCRIPTION OF THE INVENTION

Platinum on palladium core-shell nanostructures, methods for producingsuch core-shell nanostructures, and their use as electrocatalysts inoxygen reduction reaction (ORR) are described herein.

I. Definitions

“Adatom”, as used herein, refers to atoms associated with (e.g.,adsorbed to) a crystal surface of a substrate.

“Conformal,” as used herein refers to the ability of a metal layer toassume intimate contact with an underlying surface topography onto whichit is deposited.

“Core-shell,” as used herein refers to a nanostructure which is denotedas “X@Y_(nL),” referring to, for example, a core-shell nanostructurewherein the particle has a core of X and a shell of Y; n denotes thenumber of overlayers of Y and “L” is an abbreviation of the term layers.The platinum on palladium core-shell nanostructures described herein aredenoted as Pd@Pt_(nL).

“Catalyst,” as used herein, refers to core-shell nanostructures thathave catalytic activity, such as for oxygen reduction reaction (ORR).

“Nano-substrate,” or “seeds,” are used interchangeably and herein referto a nano-scale metal object, typically formed of palladium.

“Core-shell nanostructure,” as used herein, refers to a nano-scalecore-shell particle formed of a metallic core, typically palladium,having one or more shells or overlayers of another metal, typicallyplatinum. The core-shell nanostructures can also be consideredcore-shell nanoparticles.

“Electrocatalyst,” as used herein, refers to a catalyst thatparticipates in an electrochemical reaction. Such catalyst materialsmodify and increase the rate of chemical reactions without beingconsumed in the process.

“Electrochemically active surface area (ECSA)” of the catalyst, as usedherein, refers to the surface area of the catalyst which contacts theelectrolyte and participates in electrochemical reactions.

“Overlayers,” as used herein, refers to about one or more atomic layersof metal atoms which occupy the available surface sites and cover theexposed surface of a substrate. When more than one layer is present onthe surface, each layer is epitaxially deposited layer-by-layer on topof a preceding layer. When the surface coverage does not fully cover thesubstrate surface the overlayer is considered to be a submonolayer.

“Perfect,” as used herein, refers to a nano-substrate or core-shellnano-structure wherein the tips, vertices, edges, and/or corners aresharp.

“Truncated,” as used herein, refers to a nano-substrate or core-shellnano-structure wherein the tips, vertices, corners, and/or edges showany degree of truncation.

II. Methods of Making Core-Shell Nanostructures A. Preparation ofPalladium Nano-Substrates

Palladium nano-substrates (seeds) can be produced by conventionalmethods known in the art. Palladium nano-substrates are used as seedsonto which epitaxial layer-by-layer deposition of zero-valent platinumoverlayers is applied.

In one embodiment, nano-substrates (seeds) are prepared by contacting apalladium-containing compound with a reducing agent in a suitablesolvent Exemplary palladium-containing compounds include, but are notlimited to, palladium(II) chloride, palladium(II) bromide, palladium(II)iodide, palladium(II) nitrate, sodium tetrachloropalladate(II),potassium tetrachloropalladate(II), potassium hexachloropalladate(IV),ammonium tetrachloropalladate(II), ammonium hexachloropalladatea(IV),palladium(II) acetate, palladium(II) acetylacetonate, palladium(II)hexafluoreacetylacetonate, palladium(II) trifluoroacetate,tetraamminepalladium(II) acetate, tetraamminepalladium(II) nitrate,tetraamminepalladium(II) sulfate, tetraamminenalladium(II) dichloride,bis(acetonitrile) dichloropalladium(II), andbis(benzonitrile)palladium(II) chloride. In one preferred embodiment,the palladium-containing compound is sodium tetrachloropalladate(II).

Typically, the palladium-containing compound is dissolved in a suitablesolvent to form a solution which is added to a separate solutioncontaining the reducing agent, in some embodiments, the molarconcentration of the palladium-containing compound solution prepared isin the range of about 0.1 to about 1000 mmol L⁻¹, more preferably about1.0 to about 100 mmol L⁻¹. Those skilled in the art will appreciate thatthe molar concentration of the palladium-containing compound solutioncan be adjusted to any concentration needed for the purposes of scalingup the synthesis.

Exemplary reducing agents include, but are not limited to L-ascorbicacid, citric acid, formaldehyde, formic acid, poly(vinyl pyrrolidone),sodium citrate, glucose, ethylene glycol, diethylene glycol, triethyleneglycol, tetraethylene glycol, and polyethylene glycol. The molar ratioof reducing agent added in relation to the amount ofpalladium-containing compound is as least about 1:1, at least about1.2:1, at least about 1.3:1 or at least about 1.5:1. In one preferredembodiment, the reducing agent is L-ascorbic acid and thepalladium-containing compound is sodium tetrachloropalladate(II). Inanother preferred embodiment, the reducing agent is formaldehyde and thepalladium-containing compound is sodium tetrachloropalladate(II). In yetanother preferred embodiment, the reducing agent diethylene glycol (DEG)and the palladium-containing compound is sodiumtetrachloropalladate(II).

In preferred embodiments, one or more colloidal stabilizers, such aspoly(vinyl pyrrolidone) (PVP), cetrimonium bromide (CTAB), cetrimoniumchloride (CTAC), organic acids and organic amines andpoly(diallyldimethylammonium chloride), and/or capping agents, such asbromide ions formed from potassium bromide (KBr), sodium bromide (NaBr)or ammonium bromide (NH₄Br) are added during the synthesis of thepalladium nano-substrates (seeds) according to the method disclosedherein.

Suitable solvents used to prepare the solutions described above can bechosen from polar or non-polar aqueous or organic solvents. In certainembodiments, the suitable solvent is a polyol-type solvent. Exemplarypolyol-type solvents include, but are not limited to ethylene glycol,diethylene glycol, and tetraethylene glycol. In a preferred embodimentthe polyol solvent is ethylene glycol (EG) or diethylene glycol (DEG).In other embodiments, the solvent is water, deionized water or apredominantly aqueous solvent. In certain other embodiments the suitablesolvent is selected from one or more organic solvents such as organicacids, amines, benzyl alcohol, or dimethylformamide (DMF). The solventor solvent mixture chosen can be degassed as necessary using anyappropriate method known in the an and the reaction is typically carriedout under inert atmosphere.

The reaction to form the palladium nano-substrates can be performed at atemperature range from about 20° C. to about 150° C. and the reactioncan be carried out for any suitable amount of time required to producethe desired palladium nano-substrates, the period of time beingpreferably in the range of from about one hour to about 24 hours.

The palladium nano-substrates can be isolated using any appropriatetechnique known in the art such as, for example, filtration orcentrifugation. The isolated palladium nano-substrates can be purified,as needed, by washing any number of times with deionized water, and/ororganic solvents. The purified palladium nano-substrates can bere-dispersed in a suitable solvent, such as ethylene glycol or deionizedwater, and stored prior to deposition of one or more platinumoverlayers. Alternatively, the palladium nano-substrates can be driedand stored and subsequently re-dispersed in a suitable solvent (i.e.,ethylene glycol or deionized water) prior to deposition of one or moreplatinum overlayers.

The palladium nanosubstrates produced according to the method describedcan have a shape chosen from the group consisting of cubic, tetrahedral,bipyramidal, octahedral, icosahedral, decahedral, concave cubic, plate,rod and wire shapes. In certain embodiments the aforementionednano-substrate shapes are non-truncated (perfect) or they are truncated,having various degrees of truncation at the corners and/or edges. Incertain other embodiments, the nano-substrates seeds can be rod (i.e.,rectangular, pentagonal, octagonal), bar (i.e., rectangular), wire(i.e., rectangular, octagonal, pentagonal), and plate shaped. Theselection of shape and/or degree of truncation can be controlledaccording to the reaction conditions used.

The average particle size of the palladium nano-substrates (seeds)produced is preferably in the range of about 1 to about 1000 nm, asmeasured from the edge lengths of the nano-substrates. The size of thepalladium nano-substrates (seeds) can be controlled according to thereaction conditions used.

B. Deposition of Platinum Overlayers onto Palladium Nano-Substrates

The palladium nano-substrates discussed above act as seeds onto whichone or more epitaxially deposited overlayers of zero-valent platinum areformed to produce platinum on palladium nanostructures, denotedPd@Pt_(nL), wherein the value of “n” denotes the number of platinumoverlayers and “L” is an abbreviation of the term layer(s).

Generally, the palladium nano-substrates as discussed above have a shapeselected from cubic, tetrahedral, bipyramidal, octahedral, icosahedral,and decahedral shapes or, alternatively, have a rod (i.e., rectangular,pentagonal, octagonal), bar (i.e., rectangular), wire (i.e.,rectangular, octagonal, pentagonal), or plate shape and the selectedshape can perfect (non-truncated) or truncated, having any degree oftruncation at the corners and/or edges. Preferred palladiumnano-substrates have cubic, octahedral, or icosahedral shapes, which mayor may not be truncated. Preferably, the palladium nano-substratecrystals are enclosed by {111} and/or {100} facets and/or have twindefects on the nano-substrate surface.

According to the method described herein, core-shell nanostructuresformed of a palladium nano-substrate core conformally coated with one ormore overlayers of epitaxially deposited zero-valent platinum atoms areproduced by a method including the steps of:

(1) combining a first solution comprising a plurality of palladiumnano-substrates and a reducing agent with a second solution comprising aplatinum-containing compound; and

(2) heating the mixture to induce epitaxial layer-by-layer deposition ofone or more platinum overlayers conformally deposited onto the palladiumnano-substrates.

Exemplary reducing agents include, but are not limited to L-ascorbicacid, citric acid, formaldehyde, formic acid, poly(vinyl pyrrolidone),sodium citrate, glucose, ethylene glycol, diethylene triethylene glycol,tetracthylene glycol, and polyethylene glycol. The molar ratio ofreducing agent added to in relation to amount of platinum-containingcompound is as least about 1:1, at least about 1.2:1, at least about1.3:1 or at least about 1.5:1. In one preferred embodiment, the reducingagent is L-ascorbic acid. In another preferred embodiment, the reducingagent is citric acid.

In certain embodiments, the platinum-containing compound is selectedfrom the group consisting of platinum(II) chloride, platinum(IV)chloride, platinum(II) bromide, chloroplatinic acid, sodiumtetrachloroplatinate(II), sodium hexachloroplatinate(IV), potassiumtetrachloroplatinate(II), potassium hexachloroplatinate(IV),tetraammineplatinum(II) chloride, tetraammineplatinum(II) nitrate,ammonium tetrachloroplatinate(II), ammonium hexachloroplatinate(IV),platinum(II) acetylacetonate, and hydrates thereof. In some embodiments,the platinum-containing compound is sodium hexachloroplatinate(IV). Inanother preferred embodiment, the platinum-containing compound ispotassium tetrachloroplatinate(II).

Typically, the platinum-containing compound is dissolved to form aseparate solution which is added to the solution containing theplurality of palladium nano-substrates and reducing agent. In someembodiments, the molar concentration of the platinum-containing compoundsolution prepared is in the range of about 0.1 to about 1000 μmol L⁻¹,more preferably about 1.0 to about 100 μmol L⁻¹. Those skilled in theart will appreciate that the molar concentration of theplatinum-containing compound solution can be adjusted to anyconcentration as needed for purposes of scaling up the synthesis. Theconcentration of palladium nano-substrates in the first solutionprepared is typically in the range of about 0.01 to about 2.0 mg mL⁻¹.Those skilled in the art will appreciate that the concentration of thesolution containing the palladium nano-substrates can be adjusted to anyconcentration as needed for the purposes of scaling up the synthesis.The volume of the platinum-containing compound solution added to thesolution containing the dispersed palladium nano-substrates and reducingagent can be used as a parameter to control the number of zero-valentplatinum overlayers deposited on the palladium nano-substrates. In someembodiments, the platinum-containing second solution is added to thefirst solution containing the dispersed palladium nano-substrates andreducing agent in its entirety in one single shot addition. In otherembodiments, the solution of the platinum-containing compound can beadded (injected) to the solution containing the dispersed palladiumnano-substrates and reducing agent at a rate selected from the range ofabout 0.5 to about 100 mL h⁻¹, more preferably about 1.0 to about 75 mLh⁻¹, and most preferably about 3.0 to about 50 mL h⁻¹. In a preferredembodiment, the addition (injection) rate is about 4.0 mL h⁻¹. Withoutwishing to be bound by any theory, by controlling the rate of addition(injection) of the platinum containing solution, the concentration ofreduced platinum atoms can be controlled and the concentration kept to alow level which can effectively prevent self-nucleation of the newlygenerated platinum atoms. The rate of addition (injection) of theplatinum-containing solution can be controlled by any means known in theart, such as for example using a syringe pump.

Any of the solutions discussed above can be prepared in a suitablesolvent chosen from polar or non-polar aqueous or organic solvents. Incertain embodiments, a preferred solvent is a polyol-type solvent.Exemplary polyol-type solvents include, but axe not limited to ethyleneglycol, diethylene triethylene glycol, and tetraethylene glycol. In apreferred embodiment the polyol solvent is ethylene glycol. In otherembodiments, the preferred solvent water, deionized water, or apredominantly aqueous solvent. In certain other embodiments the suitablesolvent is chosen from one or more organic solvents selected from thegroup consisting of organic acids, amines or benzyl alcohol. The solventor solvent mixture chosen can be degassed as necessary using anyappropriate method known in the art and the platinum deposition processaccording to the method is typically carried out under inert atmosphere.

In some embodiments, one or more colloidal stabilizers, such as PVPand/or capping agents, such as bromide ions from KBr, NaBr, or NH₄Br areadded during the synthesis of the Pd@Pt_(nL) core-shell nanostructuresaccording to the method disclosed herein. In certain embodiments, theone or more colloidal stabilizers, such as PVP and/or capping agents,such as bromide ions from KBr may be excluded from the synthesisaccording to the method disclosed herein.

The conformal deposition of one or more zero-valent platinum overlayersonto palladium nano-substrates is performed at an elevated temperaturein the range from about 75° C. to about 250° C. and is carried out forany suitable period of time required to produce the desired palladiumnano-substrates, the period of time preferably in the range of fromabout one hour to about 24 hours. In some embodiments, the firstsolution containing the palladium nano-substrates and reducing agent isfirst pre-heated to a temperature in the range of about 75 to about 250°C. prior to the addition of the solution of the platinum-containingcompound.

Without wishing to be bound by any theory, conformal deposition ofreduced platinum atoms on the palladium nano-substrates includes aninitial deposition of the platinum adatoms at corners of thenano-substrates believed to occur due to chemisorption of bromide ioncapping agent on side faces of palladium nano-substrates. Surfacedeposited platinum adatoms then diffuse from the corners to the edgesand side faces of the palladium nano-substrates. As a result, themorphology of the final core-shell nanostructures was largely determinedby the difference in rates responsible for platinum atom deposition(V_(deposition)) and surface diffusion of the adatoms (V_(diffusion));see FIG. 1 . A flat surface could be achieved for the zero-valentplatinum overlayers formed on the side face of a palladiumnano-substrate (seed) via a combination of slow injection of theplatinum-containing compound solution to afford a low V_(deposition)rate and high reaction temperature to afford a high V_(diffusion) rate.High reaction temperatures selected from the above temperature rangesabove provide adequate thermochemical energy to overcome (break) thehigh intrinsic surface free energy and interatomic bond energy (307 kJmol⁻¹) between platinum atoms (i.e., strong Pt—Pt interaction) in orderto induce platinum deposition by layer-by-layer epitaxy by promotingsurface diffusion of reduced platinum particles being deposited on thepalladium nano-substrates surface(s). Thus, when deposition of reducedplatinum atoms occurs more slowly than surface diffusion (i.e.,V_(deposition)<V_(diffusion)), the platinum atoms can evenly spreadacross the platinum nano-substrate side face to generate a Pd@Pt_(nL)core-shell nanostructure with a well-controlled number of platinumatomic overlayers. In contrast, when the deposition of reduced platinumatoms occurs at a rate faster than surface diffusion (i.e.,V_(deposition)>V_(diffusion)), the deposition of the platinum atoms canbe preferentially induced at the corner sites due to the lower surfacediffusion rate. Capping, agents, such as KBr used to generate bromideions in the reaction solution are important as they lower the surfacefree energy of the newly deposited platinum facets.

The Pd@Pt_(nL) nanostructures can be isolated using any appropriatetechnique known in the art such as, for example, filtration orcentrifugation. The isolated Pd@Pt_(nL) nanostructures can be purified,as needed, by washing any number of times with water, deionized water,and/or organic solvents. The purified palladium nano-substrates can bere-dispersed in a suitable solvent such as ethylene glycol or deionizedwater and stored prior to deposition of one or more platinum overlayers.Alternatively, the Pd@Pt_(nL) nanostructures can be dried and stored andsubsequently re-dispersed in a suitable solvent (i.e., ethylene glycolor deionized water) prior to deposition of one or more platinumoverlayers.

The average size of the Pd@Pt_(nL) core-shell nanostructures producedaccording to the methods described herein is preferably in the range ofabout 1 to about 1000 nm, as measured from the edge lengths of thecore-shell nanostructures. The size of the Pd@Pt_(nL) core-shellnanostructures can be controlled according to the reaction conditionsused.

1. Platinum Overlayer Deposition in Polyol-Based Solvent

According to one embodiment, the deposition of one or more zero-valentplatinum overlayers onto palladium nano-substrates can be carried out ina polyol-type solvent, such as ethylene glycol (EG), and the reactionsolution is preferably heated to a temperature in the range of about 150to about 250° C., more preferably about 175 to about 225° C., and mostpreferably 190 to about 210° C. In a preferred embodiment, thedeposition of zero-valent platinum overlayers in a polyol solvent iscarried out at about 200° C.

In some embodiments, the weight percentage of platinum in the Pd@Pt_(nL)nanostructures is from about 1% to about 50%, from about 10% to about45%, from about 20% to about 35%, depending on the number of zero-valentplatinum overlayers.

2. Platinum Overlayer Deposition in an Water-Based Solvent

According to another embodiment, the deposition of one or morezero-valent platinum overlayers onto palladium nano-substrates iscarried out in an solvent, such as deionized water, and the reactionsolution is preferably heated to a temperature in the range of about 75to about 100° C., more preferably about 90 to about 95° C. In apreferred embodiment, the deposition of zero-valent platinum overlayersin an aqueous solvent is carried at about 95° C. in the case ofaqueous-based synthesis of Pd@Pt_(nL) core-shell nanostructures,sharpening of corners for the core-shell nanostructures may occur due tothe use of the lower temperature employed, relative to the synthesis ofsuch nanostructures at higher temperatures, such as in the polyol-basedsolvent system; see FIG. 2 .

To preclude/inhibit self-nucleation of platinum atoms at the relativelylower reaction temperature range of about 100° C., a mild reducingagent, such as citric acid was preferentially used. The use of a mildreducing agent can result in a low concentration of free reducedplatinum atoms in the reaction solution which suppressesself-nucleation. Moreover, the use of a mild reducing agent permits theaddition of the (precursor) solution of a platinum-containing compoundas one single shot. One of ordinary skill in the art would be able toreadily select a suitable reducing agent which has mild reducingproperties.

In preferred embodiments, no capping agents, such as potassium bromide(KBr) are added during the synthesis of the Pd@Pt_(nL) core-shellnanostructures in an aqueous solvent.

In some embodiments, the weight percentage of platinum in the Pd@Pt_(nL)nanostructures is from about 1% to about 50%, from about 10% to about45%, from about 20% to about 35% depending on the number of zero-valentplatinum overlayers deposited.

III. Pd@Pt_(nL) Core-Shell Nanostructures

The Pd@Pt_(nL) core-shell nanostructures synthesized according themethods described herein are formed from a palladium nano-substrate corewhich is conformally coated with one or more atomic overlayers ofepitaxially deposited zero-valent platinum atoms.

The Pd@Pt_(nL) core-shell nanostructures typically adopt the shape ofthe palladium nano-substrate (seed) on to which the one or morezero-valent overlayers were deposited onto. The Pd@Pt_(nL) core-shellnanostructures may have a shape selected from cubic, concave cubic,tetrahedral, bipyramidal, octahedral, icosahedral, decahedral, rod, bar,wire, and plate shapes. The produced Pd@Pt_(nL) core-shellnanostructures can have a perfect shape or have corners and/or edgeswhich show any degree of truncation. In some embodiments, the reactionconditions can affect the sharpness of the corners of the Pd@Pt_(nL)core-shell nanostructures produced; see FIG. 2 . For example, in anaqueous solvent system using a mild reducing agent at a temperature ofabout 95° C., it was found that deposition of platinum overlayersresulted in sharp corners. In some embodiments, the above-describedshapes of the Pd@Pt_(nL) core-shell nanostructures are concave innature.

In preferred embodiments, the Pd@Pt_(nL) core-shell nanostructuresproduced have about one to about ten atomic overlayers of zero-valentplatinum deposited onto them typically via epitaxial layer-by-layergrowth. The one or more zero-valent platinum overlayers formed areuniformly deposited and can form smooth surfaces on the coated palladiumnano-substrates (seeds). In certain embodiments, the entire surface ofthe nano-substrate covered by a continuous and uniform shell of the oneor more platinum overlayers deposited.

In some embodiments, the palladium nano-substrate crystal has {100},{111} facets and/or twin defects on its surface such that the one ormore zero-valent platinum overlayers formed on the palladiumnano-substrate generate a corrugated surface morphology. Without wishingto be bound by any theory, when lateral relaxation on the {111} facet ofthe palladium nano-substrate is constrained by twin boundaries, theplatinum adatoms can only relax along a direction normal to thepalladium nano-substrate surface thereby generating a corrugatedoverlayer(s) on the core-shell nanostructure.

The Pd@Pt_(nL) core-shell nanostructures can have an average particlesize in the range of about one to about 1000 nm, more preferably aboutone to about 100 nm. The platinum-coated particles can be approximately,or precisely, monodisperse in size. Alternatively, the particles can beanywhere from slightly to widely polydisperse in size.

The Pd@Pt_(nL) core-shell nanostructures can have a weight percentage ofplatinum from about 1% to about 50%, from about 10% to about 45%, fromabout 20% to about 35%, depending on the number of zero-valent platinumoverlayers deposited.

IV. Electrocatalytic Applications Using Pd@Pt_(nL) Nanostructures

In certain embodiments, the Pd@Pt_(nL) core-shell nanostructuresdescribed herein are used as electrocatalysts for oxygen reductionreaction (ORR). In certain other embodiments, the Pd@Pt_(nL) core-shellnanostructures described herein can be used as electrocatalysts forhydrogen oxidation reaction (HOR). For example, the Pd@Pt_(nL)core-shell nanostructures can be used in fuel cell applications, such asin a proton-exchange membrane fuel cell (PEMFC), wherein the followingreactions occur at the respective electrodes:2H₂→4H⁺+4e ⁻  Hydrogen Oxidation Reaction (at anode):O₂+4H⁺+4e ⁻→2H₂O  Oxygen Reduction Reaction (at cathode):

The Pd@Pt_(nL) core-shell nanostructures described herein can beincorporated into an electrode of a fuel cell, such as a proton exchangemembrane fuel cell (PEMFC), to improve the performance of the fuel cell.The Pd@Pt_(nL) core-shell nanostructures, when used as electrocatalystsfor oxygen reduction reaction (ORR) and/or hydrogen oxidation reaction(HOR), can produce notable enhancements in specific and mass activities,as compared to a commercial PVC catalyst.

Generally, a fuel cell will include a first electrode, a secondelectrode, an electrolyte between the first electrode and the secondelectrode, and a proton exchange membrane between the electrodes. Insome embodiments, a first electrode contains the Pd@Pt_(nL) core-shellnanostructures. In certain embodiments, both the first and secondelectrodes may contain the Pd@Pt_(nL) core-shell nanostructures. Theskilled artisan may construct PEM fuel cells and select components ofthe fuel cells, such as electrolytes and membranes based on knowledgeavailable in the art.

The Pd@Pt_(nL) core-shell nanostructures as described herein can beloaded on to an electrically conductive support to form an(electro)catalyst composition according to any suitable method known. Inpreferred embodiments, the electrically conductive support iscarbon-based. Exemplary carbon-based electrically conductive supportsinclude carbon, graphite, carbon nanotubes, carbon nanofibers,mesoporous carbon, graphene, Vulcan™ XC72, XC72R, BP2000, acetyleneblack, and Ketjen black, in some embodiments, the loading of thePd@Pt_(nL) core-shell nanostructures onto the conductive support is inthe range of about 0.5 to about 30 weight percent, more preferably about1.0 to about 20 weight percent.

The electrocatalyst prepared can be incorporated into an oxygen-reducingcathode of a fuel cell by any method known in the art. For example, theelectrocatalyst can be incorporated by coating an electrode (i.e.,glassy carbon electrode) with the electrocatalyst in a suitable binderand incorporating the coated electrode as an oxygen-reducing cathode inthe fuel cell. The binder can be, for example, tetrafluoroethylene-basedor perfluorinated vinyl ethers such as NAFION®. The binder can be aproton-conducting material which is derivatized with acidic groups, suchas sulfonic, carboxylic, phosphinic, or boric acid groups.

The electrochemically active surface area (ECSA) of the Pd@Pt_(nL)core-shell nanostructures on a conductive support electrocatalysts canbe derived from the charges responsible for H_(upd) desorption between agiven potential range and normalized to the platinum mass. In oneembodiment, ECSA is calculated by measuring the charges (Q_(H))generated from the desorption of hydrogen between 0.08 and 0.45 V (vs.RHE) with a reference value (210 μC cm⁻² or 240 μC cm⁻², dependent onthe facets of catalysts) for the desorption of a monolayer of hydrogenfrom a platinum surface and then dividing by the mass of platinum loadedon the working electrode. Details on the methods for determiningspecific ECSA are known in the art. The specific ECSA of the Pd@Pt_(nL)core-shell nanostructures is preferably at least about 10 m² per gram ofplatinum in the core-shell nanostructure. In some embodiments, thespecific ECSA of the nanostructures is the range of from about 15 to 125m² per gram of platinum in the core-shell nanostructures.

The mass activity at given potential at room temperature (vs. RHE) forthe Pd@Pt_(nL) core-shell nanostructure on a conductive supportelectrocatalysts is preferably at least about 0.1 A per mg of platinum.In other embodiments, the mass activity is in the range of 0.1 to about1.0 A mg⁻¹ _(Pt). In some embodiments, the mass activity at 0.9 V (vs.RHE) is the range from about 0.1 to about 1.0 A mg⁻¹ _(Pt).

In some embodiments, the Pd@Pt_(nL) core-shell nanostructures on aconductive support have improved long-term stability, as compared tostate-of-the-art commercial Pt/C catalysts, when used aselectrocatalysts in a fuel cell operating at or near room temperature orsignificantly above room temperature (i.e., greater than 50° C.).

EXAMPLES

Materials and General Methods:

Ethylene glycol (EG, 99%) was purchased from J. T. Baker. Sodiumpalladium (II) tetrachloride (Na₂PdCl₄, 99.998%) sodium hexachloroplatinate(IV) hexahydrate (Na₂PtCl₆.6H₂O, 98%), potassiumtetrachloroplatinate(II) (K₂PtCl₄, 99.99%), poly(vinyl pyrrolidone)(PVP, M_(w)≈55,000), formaldehyde (Fisher Scientific), L-ascorbic acid(99%), citric acid (99.5%), potassium bromide (KBr, 99%), diethyleneglycol (DEG), ethanol, isopropanol, and Nation® (5% solution) were allpurchased from Sigma-Aldrich and used as received. All aqueous solutionswere prepared using deionized (DI) water with a resistivity of 18.2MΩ·cm.

Structural and Compositional Analyses:

Transmission electron microscopy (TEM) images were taken using aJEM-1400 microscope (JEOL, Tokyo, Japan) or HT7700 microscope (Hitachi)operated at 120 kV by drop casting the core-shell nanostructuresdispersions on carbon-coated Cu grids and drying under ambientconditions. High-angle annular dark-field scanning transmission electronmicroscopy (HAADF-STEM) and energy dispersive X-ray (EDX) analyses wereperformed using a JEOL ARM200F microscope with STEM Cs correctoroperated at 200 kV or on an aberration-corrected FEI TitanS 80-300TEM/STEM operated at 300 kV, with a probe convergence angle of 30 mradand a large inner collection angle of 65 mrad and a JEOL JEM 2200FSSTEM/TEM microscope equipped with a CEOS probe corrector (Heidelberg,Germany).

Quantitative analysis of metal content composition of theplatinum-palladium nanostructures was determined by inductively coupledplasma mass spectrometry (ICP-MS; NexION 300Q, Perkin Elmer).

Preparation of Palladium Nano-Substrates (Seeds):

Pd nanocube seeds with an average edge length of 18 nm were synthesizedaccording to a previously reported protocol (Sin, M. et al. Nano Res.2011, 83-91). In a typical synthesis, PVP (105 mg), L-ascorbic acid (60mg), KBr (600 mg), and 8.0 mL of deionized water (18.2 MΩ·cm) were mixedin a 25 mL vial and pre-heated at 80° C. for 10 min in an oil bath undermagnetic stirring. Na₂PdCl₄ (57 mg) was separately dissolved in DI water(3 mL) and then added into the pre-heated solution. The reaction vialwas capped and maintained at 80° C. for an additional 3 hours. The finalproduct was collected by centrifugation, washed (3×) with DI water, andsubsequently re-dispersed in EG (11 mL).

Pd nano-octahedra seeds of 15 and 19 am in edge length were synthesizedaccording to a previously reported protocol (Jin, M. et al. EnergyEnviron. Sci. 2012, 5, 6352-6357) from Pd cubes of 6 and 10 nm in edgelength, respectively, the cubes having been prepared according to apreviously reported protocol (Jin, M. et al. Nano Res. 2011, 4, 83-91).Briefly, for the synthesis of Pd octahedra, a suspension of the Pdnanocubes (0.3 mL, 1.8 mg mL⁻¹), and formaldehyde (0.1 mL) were addedinto an aqueous solution (8 mL) containing PVP (105 mg) and the mixturewas heated at 60° C. for 10 min under magnetic stirring. An aqueoussolution (3 mL) containing Na₂PdCl₄ (29 mg) was then quickly added intothe pre-heated solution. The reaction solution was kept at 60° C. for 3hours under magnetic stirring. The reaction solution was subsequentlycooled to room temperature. The Pd octahedra products were collected bycentrifugation, washed with DI water (2×), and re-dispersed in EU (2 mL)or DI water (10 mL).

Pd nano-icosahedra seeds were synthesized according to a modifiedreported protocol (Lv, T. et al. ChemSusChem 2013, 6, 1923-1930).Briefly, PVP (80 mg) was dissolved in 2.0 ml of DEG in a 20 mL vial andthe solution was heated at 130° C. in an oil bath under magneticstirring for 10 min. Concurrently, Na₂PdCl₄ (15.5 mg) was dissolved in1.0 mL DEG and the solution was injected in one shot into the pre-heatedsolution with a pipette. The vial was capped and heating at 130° C. wascontinued for 3 h. The product was collected by centrifugation, washedwith acetone (1×) and DI water (2×) to remove excess PVP and inorganicions, and subsequently re-dispersed in 3 mL of EG.

Example 1: Preparation of Pd@Pt_(nL) (N=1-6) Nanocubes

For the synthesis of Pd@Pt_(nL) (n=1-6) nanocubes, 1.0 mL of the 18 nmcubic Pd seed dispersion (1.68 mg/mL, as determined from ICP-MS and TEMmeasurements), L-ascorbic acid (100 mg), KBr (54 mg), PVP (66.6 mg), and12 mL of EG were mixed in a 50 mL flask and pre-heated at 110° C. for 1hour. The reaction temperature was then quickly ramped up to 200° C.within a 10 min period. Subsequently, the deposition of the Pt atomiclayers was initiated by injection of a given volume of a Na₂PtCl₆.6H₂Osolution in ethylene glycol (0.25 mg mL⁻¹) into the pre-heated reactionsolution at a relatively slow rate of 4.0 mL h⁻¹ (˜10.0 μL per droplet).After the injection of a specific amount of the platinum precursor, thereaction solution was kept at 200° C. for another 1 hour. The finalPd@Pt_(nL) nanocubes were collected by centrifugation, washed ethanol(2×) and DI water (3×), and subsequently redispersed in DI water.

Characterization of Pd@Pt_(nL) Nanocubes:

The number of platinum atomic overlayers was controlled as a function ofthe volume of platinum precursor (i.e., Na₂PtCl₆.6H₂O solution) added tothe palladium nanocube seeds. Quantitative analysis of the averagenumber (n) of platinum atomic layers on the Pd@Pt_(nL) nanocubes andweight percent of platinum in the nanocubes was determined usinginductively coupled plasma mass spectrometry (ICP-MS) as shown in Table1 below.

TABLE 1 Pt content of Pd@Pt_(nL) nanocubes. n of Pt Weight percent ofatomic Pt calculated from Sample layers ICP-MS data Pd@Pt_(1L) 1 11.6Pd@Pt_(2-3L) 2-3 23.1 Pd@Pt_(4L) 4 33.9 Pd@Pt_(6L) 6 44.0

HAADF-STEM images of Pd@Pt_(nL) (n=1, 4, and 6) nanocubes are shown inFIG. 3 . During the deposition of platinum atomic overlayers, the cubicshape of the palladium substrate seeds was retained, and the overlayersproduced were flat and conformal with smooth surfaces as shown,indicating the involvement of epitaxial layer-by-layer growth. TheHAADF-STEM imaging showed good contrast between the platinum overlayershell and the palladium core. The Pd@Pt_(nL) core-shell nanocubes had anaverage edge length of 19.2 nm, which was 1.2 nm greater than that ofthe initial palladium nano-cube substrate seeds. On average, thethickness of the platinum shell deposited on each palladium {100} facewas around 0.6 nm. Based on the unit cell parameters of platinum, threeatomic layers correspond to a thickness of 0.59 nm, which is in goodagreement with the value of 0.6 nm measured from the change to averageedge length.

Energy-dispersive X-ray spectroscopy (EDX) analysis of the Pd@Pt_(nL)(n=1, 4, and 6) nanocubes taken reveal the elemental compositions of thedifferent nanocubes along the platinum overlayer shell and palladiumcore as shown in FIG. 3 .

Example 2: Preparation of the Pd@Pt_(nL) (N=2-5) Octahedra in aPolyol-Based System

For the synthesis of Pd@Pt_(nL) (n=2-5) octahedra, 1.0 mL of the Pdoctahedra EG suspension (19 nm in edge length, 0.83 mg mL⁻¹), PVP (67mg), L-ascorbic acid (100 mg), KBr (54 mg), and 12 mL of EG were mixedin a flask and heated at 110° C. for 1 hour under magnetic stirring. Thetemperature was then quickly ramped up to 200° C. within 20 min and aspecific amount of an EG solution containing Na₂PtCl₆.6H₂O (0.1 mg mL⁻¹)was added dropwise with a syringe pump at a rate of 4.0 mL h⁻¹. Aftercomplete injection, the reaction solution was kept at 200° C. for 1 hourunder magnetic stirring and subsequently cooled to room temperature. ThePd@Pt_(nL) octahedra were collected by centrifugation, washed withethanol (2×) and with DI water (3×), and subsequently re-dispersed in DIwater.

Characterization of Pd@Pt_(nL) Octahedra(Polyol-Based Protocol):

The number of platinum atomic overlayers was controlled as a function ofthe volume of platinum precursor (i.e., Na₂PtCl₆. 6H₂O solution) addedto the palladium octahedral seeds. Quantitative analysis of the averagenumber (n) of platinum atomic layers on the Pd@Pt_(nL) octahedra andweight percent of platinum in the octahedra was determined usinginductively coupled plasma mass spectrometry (ICP-MS) as shown in Table2 below.

TABLE 2 Pt content of Pd@Pt_(nL) octahedra (polyol-based protocol).Weight percent of n of Pt atomic Pt calculated from Sample layers ICP-MSdata Pd@Pt_(2-3L) 2-3 29.1 Pd@Pt_(3-4L) 3-4 36.7 Pd@Pt_(4-5L) 4-5 43.8

TEM images of Pd@Pt_(nL) (n=2-5) octahedra are shown in FIGS. 4A-C.During the deposition of platinum atomic overlayers, the octahedralshape of the palladium substrate seeds was retained, and the overlayersproduced were flat and conformal with smooth surfaces, indicating theinvolvement of epitaxial layer-by-layer growth. As shown in FIGS. 5A-E,HAADF-STEM images of the Pd@Pt_(2-3L) core-shell octahedra confirmedthat the platinum atoms were uniformly deposited on the surfaces of thepalladium substrate seeds largely preserving the truncated corners ofthe palladium seeds during the deposition of platinum layer.

Energy-dispersive X-ray spectroscopy (EDX) analysis of the Pd@Pt_(2-3L)reveal the elemental composition along the platinum overlayer shell andpalladium core as shown in FIG. 5F.

Example 3: Preparation of the Pd@Pt_(nL) (N=2-3) Octahedra in aWater-Based Solvent

For the synthesis of Pd@Pt_(nL) (n=2-3) octahedra, PVP (35 mg) andcitric acid (60 mg) were added into 10 mL of the aqueous suspension ofthe Pd octahedra (15 nm, 0.19 mg mL⁻¹) and then heated at 95° C. for 10min wider magnetic stirring. Separately, K₂PtCl₄ (13 mg) was dissolvedin 3 mL of DI water and the solution was quickly added into thepre-heated solution using a pipette. The reaction solution was kept at95° C. for 24 hours under magnetic stirring and subsequently cooled downto room temperature. The Pd@Pt_(nL) (N=2-3) octahedra were collected bycentrifugation, washed with DI water (3×), and subsequently re-dispersedin DI water.

Characterization of Pd@Pt_(nL) Octahedra (Water-Based Protocol):

High-angle annular dark-field scanning TEM (HAADF-STEM) images ofPd@Pt_(2-3L) octahedra are shown in FIGS. 6A-E. During the deposition ofplatinum atomic overlayers, the overlayers produced were uniformlyepitaxially deposited and had smooth surfaces. The platinum atoms wereevenly deposited on all the side faces of an octahedron-shaped palladiumseed, with an average platinum shell thickness of 2-3 atomic overlayers.Pd@Pt_(2-3L) octahedra were found to have sharp corners. This suggestedthat the decreased reaction temperature in the water-based protocol canslow the rate of diffusion of the platinum adatoms from the palladiumseed corners to the side faces.

Quantitative analysis of the average number (n) of platinum atomiclayers on the Pd@Pt_(nL) octahedra and weight percent of platinum in theoctahedra was determined using inductively coupled plasma massspectrometry (ICP-MS) as shown in Table 3 below.

TABLE 3 Pt content of Pd@Pt_(nL) octahedra (water-based protocol).Weight percent of n of Pt atomic Pt calculated from Sample layers ICP-MSdata Pd@Pt_(2-3L) 2-3 29

Energy-dispersive X-ray spectroscopy (EDX) analysis of the Pd@Pt_(2-3L)octahedra reveal the elemental composition along, the platinum overlayershell and palladium core as shown in FIG. 6F.

Example 4: Preparation of the Pd@Pt_(nL) (N=0.7-4.3) Icosahedra

For the synthesis of Pd@Pt_(nL) (n=0.7-4.3) icosahedra, 1.0 mL of the Pdicosahedra (0.59 mg mL⁻¹, as determined using ICP-MS), KBr (54 mg), PVP(66 mg), L-ascorbic acid (32 mg), and 9 mL of EG were mixed in a 50-mLflask and pre-heated at 1.10° C. for 1 hour. The reaction temperaturewas then quickly ramped to 200° C. within 10 min. The deposition of Ptatomic layers was initiated by pumping a given volume of a Na₂PtCl₆.6H₂Osolution (0.06 mg mL⁻¹ in EG) into the reaction solution at a rate of4.0 mL h¹. Corresponding to the samples of Pd@Pt_(0.7L), Pd@Pt_(2L), andPd@Pt_(2.7L) icosahedra, respectively, 4 mL, 12 mL and 16 mL of theprecursor solution was introduced. After the addition of a specificamount of Pt precursor was completed, the reaction solution was kept at200° C. for another 1 hour. The final Pd@Pt_(nL) icosahedra werecollected by centrifugation, washed with acetone (1×) and with ethanol(2×), and subsequently re-dispersed in DI water. A similar procedure forthe synthesis of Pd@Pt_(nL) icosahedra was carried out except that 0.5mL of the Pd icosathedra (0.59 mg mL⁻¹) was used and 21 mL of precursorsolution (0.04 mg mL⁻¹ EG) was pumped into the growth solution at therate of 4.0 mL h⁻¹.

Characterization of Pd@Pt_(nL) Icosahedra:

TEM and HAADF-STEM images of Pd@Pt_(2-3L) icosahedra are shown in FIGS.7A-F. The icosahedral shape of the palladium seed was well-preservedduring the deposition of platinum atoms. The average diameter of theicosahedral shaped palladium seeds increased from 13.4±3.2 nm to 14.9±23nm, corresponding to a shell thickness of 0.75 nm. The HAADF-STEM imagetaken of a Pd@Pt_(nL) icosahedron along one of its 2-fold symmetry axes,confirmed that the platinum atoms were deposited as a conformal, uniformshell on the surface of a palladium icosahedral seed (see FIG. 7C). Thewell-resolved twin planes indicated that the core-shell nanostructurestill had a multiply twinned structure consistent with that of anicosahedron. The HAADF-STEM imaging indicated that the platinumoverlayer shell was only three atomic layers in thickness. HAADF-STEMimaging further revealed (see FIGS. 7E & 7F) packing of platinum atomsin the overlayers did not precisely follow the underlying palladiumatoms of the core. Instead, the platinum atoms underwent relaxation andtook on a corrugated structure (see FIGS. 7G & 7H). The formation ofsuch a corrugated structure was attributed to the existence of bothtensile strain and twin boundaries on the surface of the palladiumicosahedral seed. An icosahedron consists of twenty tetrahedralsubunits, with twenty {111} facets and thirty twin boundaries on itssurface. Each {111} facet is laterally confined by three twinboundaries. Lattice expansion allows for extra platinum atoms to bepacked into each platinum overlayer relative to the number of palladiumatoms present cm the surface of the initial seed. As a result, surfacerelaxation must be involved during the conformal deposition of aplatinum shell onto the palladium icosahedral seed. Since lateralrelaxation on the {111} facet is constrained by twin boundaries, theplatinum atoms can only relax along a direction normal to the surface,thereby generating a corrugated structure.

Quantitative analysis of the average number (n) of platinum atomiclayers on the Pd@Pt_(nL) icosahedra and weight percent of platinum inthe icosahedra was determined using inductively coupled plasma massspectrometry (ICP-MS) as shown in Table 4 below. By reducing the volumeof the platinum precursor (i.e., Na₂PtCl₆.6H₂O solution) added whilefixing the amount of the palladium icosahedral-shaped seeds, theplatinum shell thickness could be readily tuned from multiple layersdown to a single or even a sub-atomic layer, as indicated by the ICP-MSdata.

TABLE 4 Pt content of Pd@Pt_(nL) icosahedra Weight percent of n of Ptatomic Pt calculated from Sample layers ICP-MS data Pd@Pt_(0.7L) 0.711.0 Pd@Pt_(2L) 2.0 27.5 Pd@Pt_(2.7L) 2.7 34.2 Pd@Pt_(4.3L) 4.3 47.0

The relative rates for atom deposition (V_(deposition)) and surfacediffusion (V_(diffusion)) affect the deposition of platinum overlayerson the palladium seeds as discussed earlier. In the present example, dueto the use of a relatively strong reducing agent like L-ascorbic acid,the platinum(IV) precursor is expected to be reduced immediately uponits introduction into the reaction (growth) solution so thatV_(deposition) is largely determined as a function of the injectionrate. For an icosahedral-shaped palladium seed, every vertex is theintersection of five twin boundaries. Therefore, the platinum atoms tendto be deposited onto the vertices of a Pd icosahedral seed and theplatinum adatoms can then diffuse to the edges and side faces of thepalladium substrate. When using a slow injection rate for the platinumprecursor (i.e., Na₂PtCl₆.6H₂O solution), the rate of V_(deposition)will be small, while a high reaction temperature (200° C.) will resultin a large rate of V_(diffusion) so that the platinum atoms deposited onthe vertices can quickly diffuse to the edges and side faces to generatea conformal, uniform shell. The deposition of Pt atoms can follow alayer-by-layer growth mode, leading to the formation of Pd@Pt_(nL)icosahedra with a well-controlled thickness for the shell. The effect ofreducing the deposition reaction temperature, for example down to 120°C., causes the surface diffusion of platinum adatoms to decelerate dueto a lower rate of V_(diffusion) and most of the deposited platinumatoms preferentially remain at the vertices and edges resulting in theformation of core-shell icosahedra with a concave surface. Increasingthe deposition reaction temperature to 140° C., causes the relativesurface diffusion to accelerate (increased V_(diffusion)) for thedeposited platinum atoms so that the extent of concaveness of thecore-shell icosahedra becomes less significant.

Example 5: Electrochemical Measurements on Pd@Pt_(nL) Nanocubes

Electrochemical measurements were conducted using a glassy carbonrotating disk electrode (RDE, Pine Research Instrumentation) connectedto a CHI 600E Potentiostat (CH Instruments). A leak free Ag/AgCl/NaCl(3M) electrode (BASi) was used as the reference. All potentials wereconverted to values with reference to a reversible hydrogen electrode(RHE). The counter electrode was a Pt mesh (1×1 cm²) attached to a Ptwire. The electrolyte was 0.1 M HClO₄ diluted from a 70% stock solution(Baker, ACS Reagent grade) with DI water.

The working electrode was prepared by loading the Pd@Pt_(nL) nanocubesonto a carbon black support (Ketjen®) with a metal loading content of 20wt % based on the total mass of Pd and Pt (as checked by ICP-MSmeasurement). The resulting Pd@Pt_(nL) nanocubes on carbon(Pd@Pt_(nL/C)) catalysts were then dispersed in acetic acid (10 mL) andheated at 60° C. for 12 hours to clean the surface of the Pd@Pt_(nL)nanocubes, and then washed with ethanol (2×). After drying, 6.0 mg ofthe Pd@Pt_(nL)/C catalyst was dispersed in a mixed solvent (2.0 mL of DIwater, 2.0 mL of isopropanol, and 80 μL of 5% Nafion®) viaultrasonication for 20 min. The suspension (20 μL) was deposited onto apre-cleaned glassy carbon rotating disk electrode (RDE) with a geometricarea of 0.196 cm² and dried in an oven preset at 60° C. Controls wereprepared from Pt/C catalysts (20 wt % 3.2-nm nanoparticles on Vulcan™XC-72 carbon support obtained directly from Premetek Co.), the workingelectrode was prepared using the same procedure except for the exclusionof the heating treatment in acetic acid. Therefore, the loading amountof metal for the Pd@Pt_(nL)/C and Pt/C catalysts was 6 μg 30.6 μg/cm²based on the geometric electrode area).

Cyclic voltammograms (CVs) were measured in a N₂-saturated 0.1M aqueousHClO₄ electrolyte by cycling between 0.08 and 1.1 V (vs. RHE) at a sweeprate of 0.05 V s⁻¹. The electrochemically active surface area (ECSA) wasestimated by measuring the charges (Q_(H)) generated from the desorptionof hydrogen between 0.08 and 0.45 V (vs. RHE) normalized to the Pt mass.

Oxygen reduction reaction (ORR) testing was carried out in anO₂-saturated 0.1 M aqueous HClO₄ electrolyte at room temperature with ascan rate of 0.01V s⁻¹ and a rotation speed of 1,600 rpm.

The kinetic current density (j_(k)) was derived from the Koutecky-Levichequation as follows:

$\frac{1}{j} = {\frac{1}{j_{k}} + \frac{1}{j_{d}}}$

where j is measured current density and j_(d) is the diffusion-limitingcurrent density.

For accelerated durability testing, CVs and ORR polarization curves weremeasured after sweeping for 5.000 and 10,000 cycles between 0.6 and 1.1V (vs. RHE) at a rate of 0.1 V s⁴ in an O₂-saturated 0.1 M aqueous HClO₄solution at room temperature.

Results:

The specific electrochemical active surface areas (ECSA) of Pd@Pt_(1L)/C(104.1 m² g⁻¹ _(Pt)) was almost twice that of the control Pt/C catalyst(51.4 m² g⁻¹ _(Pt)) and four times that of platinum nanocubes (23.9 m²g⁻¹ _(Pt)) alone. As the average number of platinum atomic overlayersincreased, the specific ECSAs were found to gradually drop to 47.6,39.7, and 24.9 m² g⁻¹ _(Pt) for the Pd@Pt_(2-3L)/C, Pd@Pt_(4L)/C, andPd@Pt_(6L)/C catalysts, respectively (see FIG. 8 ). The ECSAs of thesePd@Pt_(nL)/C (n=1-6) catalysts were all comparable to those of thecommercial Pt/C and to platinum nanocubes despite the fact that theiraverage sizes (18-21.2 nm) were much larger than those of Pt/C (3.2 nm)and of the platinum nanocubes (9 nm). The large specific ECSAsassociated with the Pd@Pt_(nL)/C (n<4) catalysts suggest an increase inutilization efficiency of the platinum atoms when these core-shellnanocubes are used as electrocatalysts.

The positive-going ORR polarization curves of the Pd@Pt_(nL)/C (n=1-6)catalysts are shown in FIG. 9 . To better understand the surface andmass effects, we calculated the kinetic currents from the ORRpolarization curves according to the Koutecky-Levich equation and thennormalized the kinetic current to the ECSA (j_(k,specific)) and platinummass (j_(k,mass)), respectively. The specific activities of thePd@Pt_(nL)/C (n≤4) catalysts were all enhanced in the potential regionbetween 0.86 and 0.94 V relative to the state-of-the-art commercial Pt/Ccatalyst and the Pt nanocubes. As shown in FIG. 10A, at 0.9 V (vs. RHE)the j_(k,specific) values of the four different Pd@Pt_(nL)/C (n=1, 2-3,4, and 6) catalysts were found to show a volcano-shaped dependence basedon the number of platinum atomic overlayers with a maximum pointcorresponding to the Pd@Pt_(2-3L)/C catalyst which was 1.6 times that ofthe platinum nanocubes.

The mass activities of the Pd@Pt_(nL) nanocubes with n=1-4 atomicoverlayers of platinum all showed substantially improved mass activitiesas compared to the state-of-the-art commercial Pt/C catalyst (see FIG.10B). The overall enhancements in platinum mass activity were attributedto (i) an improvement in the specific activity and (ii) to changes inplatinum dispersion. The specific activity follows a volcano trend,which has a maximum at 2-3 platinum atomic overlayers. However, thespecific ECSA decreases with each additional layer of platinum atoms. Assuch, by balancing these two effects, the platinum mass activity can bemaximized with only one overlayer of platinum atoms. The mass activityof Pd@Pt_(1L)/C at 0.9 V (vs. RHE) was approximately three times higherthan that of the commercial Pt/C catalyst.

The long-term stabilities of the Pd@Pt_(nL)/C catalysts were evaluatedthrough accelerated durability testing by applying linear potentialsweeps between 0.6 and 1.1 at a sweep rate of 0.1 V s⁻¹. Compared to thecontrol commercial Pt/C catalyst, the durability was greatly improved inall the Pd@Pt_(nL)/C catalysts based on the specific ECSAs and mass ORRactivities given as kinetic current densities (j_(k)) at 0.9 V (seeFIGS. 11A-B). The specific ECSAs of Pd@Pt_(2-3L)/C, Pd@Pt_(4L)/C, andPd@Pt_(6L)/C were reduced by 35%, 16%, and 12% after 10,000 cycles.Although the sizes of the Pd@Pt_(nL) nanocubes were all approximately 20nm, the specific ECSAs after the durability tests were still comparableto or even higher than that of the commercial Pt/C catalyst after 5,000cycles (FIG. 11A). At 0.9 V, the Pd@Pt_(4L)/C only showed a 6% loss inmass activity after 10,000 cycles, while losses for the Pd@Pt_(1L)/C andthe commercial Pt/C catalysts were 48% and 40% after 5,000 cycles,respectively (FIG. 11B). The increased durability of the catalystshaving thicker platinum overlayers can be attributed to improvedpassivation of the palladium cores by the platinum shells. For both thePd@Pt_(1L)/C and Pd@Pt_(2-3L)/C catalysts, most of the palladium coreswere dissolved during the durability tests and the remaining platinumatoms were noted to migrate to the corners and edges to generateplatinum cubic frames. In contrast, very few of the palladium cores weredissolved during the durability test of the Pd@Pt_(6L)/C catalysts.These results suggest a new strategy for generating platinum-basedcatalysts having excellent performance by depositing zero-valentplatinum atoms as conformally deposited and smooth ultrathin shells ontopalladium nano-substrates with relatively large sizes (e.g., >10 nm).The mass activity could be retained and even enhanced by dispersingessentially all platinum atoms on the substrate surface.

Example 6: Electrochemical Measurements on Pd@Pt_(nL) Octahedra

Electrochemical measurements were conducted using a glassy carbonrotating disk electrode (RDE, Pine Research Instrumentation) connectedto a CHI 600E Potentiostat (CH Instruments). An Ag/AgCl electrode (BAST)and a Pt mesh were used as the reference and counter electrodes,respectively. The potentials (V) were converted, to values withreference to the reversible hydrogen electrode (RHE). The electrolytewas an aqueous HClO₄ solution (Baker) with a concentration of 0.1 M.

The Pd@Pt_(nL) octahedra dispersed in water were collected bycentrifugation and re-dispersed in 20 mL of ethanol. A specific amountof carbon black (Ketjen®) was added into the suspension to obtain aloading of about 20 wt % based on the total mass of Pt and Pd. Themixture was then ultrasonicated for 3 hours and the resulting Pd@Pt_(nL)octahedra on carbon (Pd@Pt_(nL)/C) was collected by centrifugation,re-dispersed in 10 mL of acetic acid, and heated at 60° C. for 2 h toremove PVP on the surface of the particles. The Pd@Pt_(nL)/C catalystwas washed with ethanol (3×) and dried in an oven at 70° C. for 30 min.

An Pd@Pt_(nL)/C ink was prepared by adding 3 mg of the Pd@Pt_(nL)/C intoa mixture of DI water (1 mL), isopropanol (1 mL), and Nafion® (5%solution, 40 μL), followed by sonication for 10 min.

The working electrode was prepared by loading the ink (20 μL) onto aglassy carbon electrode. Another working electrode was prepared from thecarbon-supported Pt catalyst (Pt/C, 20 wt % 3.2 nm nanoparticles sinVulcan™ XC-72 carbon support, Premetek) using the same protocol.

Cyclic voltammograms (CVs) were measured in a N₂-saturated 0.1M aqueousHClO₄ electrolyte by cycling between 0.08 and 1.1 V (vs. RHE) at a sweeprate of 0.05 V s⁻¹. The electrochemically active surface area (ECSA) wasestimated by measuring the charges (Q_(H)) generated from the desorptionof hydrogen between 0.08 and 0.4 V (vs. RHE) with a reference value of210 μC cm⁻² for the desorption of a monolayer of hydrogen from a Ptsurface and then dividing by the mass of Pt loaded onto the workingelectrode.

Oxygen reduction reaction (ORR) testing was carried out in anO₂-saturated 0.1 M aqueous HClO₄ electrolyte at room temperature with ascan rate of 0.01M s⁻¹ and a rotation speed of 1,600 rpm.

The kinetic current density (j_(k)) was derived from the Koutecky-Levichequation as shown above.

For accelerated durability testing, CVs and ORR polarization curves weremeasured after sweeping for 5,000, 10,000, and 20,000 cycles between 0.6and 1.1 V (vs. RHE) at a rate of 0.1 V s⁻¹ in an O₂-saturated 0.1 Maqueous HClO₄ solution at room temperature.

Results on Pd@Pt_(nL) Octahedra (Polyol-Based):

m² g⁻¹ _(Pt)) was approximately one and half times that of the controlPt/C catalyst (51.0 m² g⁻ _(Pt)). As the average number of platinumatomic overlayers increased, the specific ECSAs were found to graduallydrop to 60.8 and 43.4 m² g⁻¹ _(Pt) for the Pd@Pt_(3-4L)/C andPd@Pt_(4-5L)/C catalysts, respectively (see FIG. 12 ). The ECSAs ofthese Pd@Pt_(nL)/C (n=2-5) catalysts were all comparable or even higheras compared to the control Pt/C catalyst, despite the fact that theiraverage sizes (21 nm) were much larger than those of Pt/C (3.2 nm).

The positive-going ORR polarization curves of the Pd@Pt_(nL)/C (n=1-6)catalysts are shown in FIG. 13 . The better understand the surface andmass effects, we calculated the kinetic currents from the ORRpolarization curves according to the Koutecky-Levich equation and thennormalized the kinetic current to the ECSA (j_(k,specific)) and platinummass (j_(k,mass)), respectively. As shown in FIG. 14A, the specificactivities of the Pd@Pt_(nL)/C catalysts all demonstrated a four-foldenhancement at 0.9 V (vs. RHE) as compared to the state-of-the-artcommercial Pt/C catalyst. Such an enhancement in the specific activitywas attributed to a combination of the enlargement in proportion of the{111} facets on the surface and the electronic coupling betweenpalladium and platinum.

As shown in FIG. 14B, the mass activities at 0.9 V (vs. RHE) of thePd@Pt_(2-3L)/C, Pd@Pt_(3-4L)/C, and Pd@Pt_(4-5L)/C based on the mass ofplatinum were 0.48, 0.40, and 0.34 A mg⁻¹ _(Pt), respectively, whichwere 5.4, 4.5, and 3.8 times higher than that of the commercial Pt/Ccatalyst (0.089 A mg⁻¹ _(Pt)). The significant improvement in the massactivity of the Pd@Pt_(nL)/C catalysts was attributed to the enhancementin both specific ORR activity and dispersion of platinum atoms. Whilethe mass activities of the Pd@Pt_(nL)/C in terms of platinum contentdecreased with an increasing number (n) of platinum overlayers, the massactivities in terms of precious metals (i.e., both platinum andpalladium) did not change significantly.

The long-term stability testing of the Pd@Pt_(nL)/C catalysts revealedsignificantly improved durability as compared to the commercial Pt/Ccatalyst. At 0.9 V (vs. RHE), the mass activity of Pd@Pt_(2-3L)/C,Pd@Pt_(3-4L)/C, and Pd@Pt_(4-5L)/C decreased by only 28.9%, 8.7%, and17.6%, respectively, after 10,000 cycles, while the mass activity of thecommercial Pt/C catalyst dropped by 54% after only 5,000 cycles (seeFIG. 15A). As shown in FIG. 15B, the changes to ORR mass activity duringthe durability testing corresponded well to the variations in specificsurface area. The ECSAs of the Pd@Pt_(2-3L)/C, Pd@Pt_(3-4L)/C, andPd@Pt_(4-5L)/C catalysts were reduced by 36.0%, 12.3%, and 12.8% after10,000 cycles. In contrast to the very small particles of the Pt/C, thePd@Pt_(nL) octahedra could be better protected from dissolution and/oragglomeration during the durability test because of their relativelylarger size. The palladium core could also inhibit the corrosion of theplatinum shell by sacrificing itself, resulting in an enhancement indurability during ORR.

Results on Pd@Pt_(nL) Octahedra (Aqueous-Based):

The specific electrochemical active surface areas (ECSA) ofPd@Pt_(2-3L)/C (53.6 m² g⁻¹ _(Pt)) was slightly higher than that of thecontrol Pt/C catalyst (51.0 m² g⁻¹ _(Pt)) as shown in FIG. 16 .

The positive-going ORR polarization curves of the Pd@Pt_(2-3L)/Ccatalyst is shown in FIG. 17 . To better understand the surface and masseffects, we calculated the kinetic currents from the ORR polarizationcurves according to the Koutecky-Levich equation and then normalized thekinetic current to the ECSA (j_(k,specific)) and platinum mass(j_(k,mass)), respectively. As shown in FIG. 18 A, the specific activityof the Pd@Pt_(2-3L)/C catalyst exhibited a five-fold enhancement at 0.9V (vs. RHE) compared to the state-of-the-art commercial Pt/C catalyst(0.91 vs. 0.17 mA cm⁻² _(Pt)). Interestingly, the specific activity ofthe Pd@Pt_(2-3L)/C catalyst prepared in an aqueous-based system washigher compared as compared to the equivalent Pd@Pt_(2-3L)/C prepared inthe polyol-based system (0.91 vs. 0.73 mA cm⁻² _(Pt)). This differencewas attributed to the fact that the nanocrystals synthesized in waterwere enclosed by well-defined {111} surfaces, while those synthesized ina polyol-based system were enclosed by a mix of {111} and {100} facetsdue to truncation at the corner sites.

FIG. 18B shows the mass activities at 0.9 V (vs. RHE) of thePd@Pt_(2-3L)/C catalyst based on the mass of platinum was 0.49 A mg⁻¹_(Pt), respectively, which was 5.5 times higher than that of the controlPt/C catalyst (0.089 A mg⁻¹ _(Pt)).

The long-term stability of the Pd@Pt_(2-3L)/C catalyst showed remarkablyimproved durability relative to the commercial Pt/C catalyst. The massactivity of the Pd@Pt_(2-3L)/C catalyst decreased by only by 13% and 46%after 10,000 and 20,000 cycles, respectively, while the mass activity ofthe commercial Pt/C catalyst dropped by 54% after only 5,000 cycles (seeFIG. 19B). The ECSA of the Pd@Pt_(2-3L)/C catalyst showed changessimilar to the ORR mass activity during the durability test (see FIG.19A). The TEM images (not shown) taken from the Pd@Pt_(2-3L)/C sampleafter the accelerated durability test suggested that the Pd cores weresacrificed during the repeated cycles of ORR due to palladium's higherreactivity than platinum.

Example 7 Electrochemical Measurements on Pd@Pt_(nL) Icosahedra

Electrochemical measurements were conducted using a glassy carbonrotating disk electrode (RDE, Pine Research Instrumentation) connectedto a CHI 600E Potentiostat (CH Instruments). A leak-free Ag/AgCl/NaCl(3M) electrode (BASi) was used as the reference. All potentials wereconverted to values with reference to a reversible hydrogen electrode(RHE). The counter electrode was a Pt mesh (1×1 cm²) attached to a Ptwire. The electrolyte was 0.1 M HClO₄ diluted from a 70% stock solution(Baker, ACS Reagent grade) with DI water.

The working electrode was prepared by loading the Pd@Pt_(nL) icosahedraonto a carbon black support (Ketjen®) with a metal loading content of 20wt % based on the total mass of Pd and Pt (as determined by ICP-MS). Theresulting Pd@Pt_(nL) icosahedra on carbon (Pd@Pt_(nL)/C) were thendispersed in 10 mL of acetic acid and heated at 60° C. for 12 h to cleanthe surface of the catalytic particles and washed with ethanol (2×).After drying, 3.0 mg of the Pd@Pt_(nL)/C catalyst was re-dispersed in amixture of DI water (1.0 mL), isopropanol (1.0 mL), and Nation® (5%solution, 40 μL), with ultrasonication for 20 min.

The working electrode was prepared by loading 20 μL of the suspensiononto a pre-cleaned glassy carbon rotating disk electrode (RDE, PineResearch instrumentation) with a geometric area of 0.196 cm² and driedin an oven pre-set to 50° C. For Pt/C catalyst (20 wt %, 3.2-nm Ptparticles on Vulcan XC-72 carbon support, Premetek Co.), the workingelectrode was prepared using similar procedure except for the exclusionof the treatment in acetic acid. The loading amounts of metal were 6 μgor 30.6 μg cm⁻², respectively, for the Pd@Pt_(nL)/C and Pt/C catalysts.

Cyclic voltammograms (CVs) were measured in a N₂-saturated 0.1M aqueousHClO₄ electrolyte by cycling between 0.08 and 1.1 V (vs. RHE) at a sweeprate of 0.05 V s⁻¹. The electrochemically active surface area (ECSA) wasestimated by measuring the charges (Q_(H)) generated from the desorptionof hydrogen between 0.08 and 0.45 V (vs. RHE) with a reference value of240 μC cm⁻² for the desorption of a monolayer of hydrogen from a Ptsurface and then dividing by the mass of Pt loaded onto the workingelectrode.

Oxygen reduction reaction (ORR) testing was carried out in an O₂saturated 0.1 M aqueous HClO₄ electrolyte at room temperature with ascan rate of 0.01V s⁻¹ and a rotation speed of 1,600 rpm.

The kinetic current density (j_(k)) was derived from the Koutecky-Levichequation as shown above.

For accelerated durability testing, CVs and ORR polarization curves weremeasured after sweeping for 5,000 and 10,000 cycles between 0.6 and 1.1V (vs. RHE) at a rate of 0.1 V s⁻¹ in an O₂-saturated 0.1 M aqueousHClO₄ solution at room temperature.

Results:

The specific electrochemical active surface areas (ECSA) ofPd@Pt_(0.7L)/C (73.9 m² g⁻¹ _(Pt)) was approximately 1.4 times that ofthe commercial PVC catalyst (51.4 m² g⁻¹ _(Pt)). As the average numberof platinum atomic overlayers increased, the specific ECSAs were foundto gradually drop to 56.3, 47.1, and 42.9 m² g⁻¹ _(Pt) for thePd@Pt_(2L)/C, Pd@Pt_(2.7L)/C, and Pd@Pt_(4.3L)/C catalysts,respectively. FIG. 20 shows the specific ECSA values of thePd@Pt_(2.7L)/C and commercial PVC catalysts. The ECSAs of thesePd@Pt_(nL)/C (n=0.7-4.3) catalysts were all comparable as compared tothe commercial Pt/C catalyst, despite the fact that their averageparticle sizes (14.9 nm) were approximately five times larger than thoseof Pt/C catalyst (3.2 nm).

The positive-going ORR polarization curves of the Pd@Pt_(nL)/C(n=0.7-4.3) catalysts are shown in FIG. 21 . To better understand thesurface and mass effects, we calculated the kinetic currents from theORR polarization curves according to the Koutecky-Levich equation andthen normalized the kinetic current to the ECSA (j_(k,specific)) andplatinum mass respectively. The specific and mass activities of thePd@Pt_(nL)/C catalysts were greatly enhanced in the potential region of0.86 to 0.94 V compared to the state-of-the-art commercial Pt/Ccatalyst. At 0.9 V (vs. RHE), the j_(k,specific) values of the differentPd@Pt_(nL)/C (n=0.7-4.3) catalysts were found to show a volcano shapeddependence based on the number of platinum atomic overlayers (see FIG.22A). For the Pd@Pt_(2.7L)/C catalyst, j_(k,specific) was 1.36 mA cm⁻²_(Pt) which was 7.8 times higher than that of the control Pt/C catalyst(0.174 mA cm⁻² _(Pt)).

The mass activity, j_(k,mass), of the Pd@Pt_(2.7L)/C catalyst was 0.64 Amg⁻¹ _(Pt) which is 7.2 times higher than that of the control Pt/Ccatalyst (0.089 A mg⁻¹ _(Pt)). The mass activities of Pd@Pt_(nL)/C(n=0.7-4.3) and commercial Pt/C catalysts are shown in FIG. 22B.

In addition to the greatly enhanced specific and mass activities, thePd@Pt_(2.7L)/C catalyst exhibited excellent thermal stability andelectrochemical durability. Under in situ heating, the corrugatedsurface of Pd@Pt_(2.7L)/C icosahedra could be well preserved even afterheating at 300° C. for 30 min (see TEM images in FIGS. 23A & 23B). Thecatalytic durability of the Pd@Pt_(2.7L)/C sample was evaluated fromboth the specific ECSAs and j_(k,mass) at 0.9 V, the catalyticdurability of the Pd@Pt_(2.7L)/C catalyst was greatly improved relativeto that of the commercial Pt/C catalyst (see FIGS. 24 A & B). After5,000 cycles, the Pd@Pt_(2.7L)/C catalyst only exhibited an 8% drop inthe specific ECSA, as opposed to the 54% drop in the ESCA of the controlPt/C catalyst after the same number of cycles. Even after 10,000 cycles,the specific ESA of the Pd@Pt_(2.7L)/C (26.5 m² g⁻¹ _(Pt)) was stillhigher than that of the commercial PVC (23.5 m² g⁻¹ _(Pt)) after only5,000 cycles. At 0.9 V, the mass activity of the Pd@Pt_(2.7L)/C catalystafter 10,000 cycles showed four-fold enhancement relative to thepristine Pt/C catalyst prior to durability test.

Unless defined otherwise, all technical and scientific terms used hereinhave the same meanings as commonly understood by one of skill in the artto which the disclosed invention belongs. Publications cited herein andthe materials for which they are cited are specifically incorporated byreference.

Those skilled in the art will recognize, or be able to ascertain usingno more than routine experimentation, many equivalents to the specificembodiments of the invention described herein. Such equivalents areintended to be encompassed by the following claims.

The invention claimed is:
 1. A fuel cell comprising a core-shellnanostructure, wherein the core-shell nanostructure comprises apalladium nano-substrate conformally coated with between one and tencontinuous uniform and smooth atomic overlayers of epitaxially depositedzero-valent platinum atoms over the whole surface of the palladiumnano-substrate, wherein the palladium nano-substrate has a shapeselected from the group consisting of cubic, concave cubic, tetrahedral,bipyramidal, octahedral, icosahedral, decahedral, rod, bar, and wire. 2.The fuel cell of claim 1, wherein the palladium nano-substrate shape isperfect or wherein edges and/or corners of the palladium nano-substrateshape are truncated.
 3. The fuel cell of claim 1, wherein the palladiumnano-substrate has {100}, {111} facets and/or twin defects on thenano-substrate surface.
 4. The fuel cell of claim 1, wherein the one toten zero-valent platinum overlayers formed on the palladiumnano-substrate have a corrugated surface morphology.
 5. The fuel cell ofclaim 1, wherein the core-shell nanostructure has a size of about one toabout one hundred nanometers.
 6. The fuel cell of claim 1, wherein thecore-shell nanostructure has a shape selected from the group consistingof cubic, octahedral, and icosahedral shapes; and the core-shellnanostructure shapes are perfect or truncated.
 7. The fuel cell of claim1, wherein the core-shell nanostructure is produced by the methodcomprising (a) combining a first solution comprising a plurality ofpalladium nano-substrates and a reducing agent with a second solutioncomprising a platinum-containing compound to form a mixture, wherein thepalladium nano-substrate has a shape selected from the group consistingof cubic, concave cubic, tetrahedral, bipyramidal, octahedral,icosahedral, decahedral, rod, bar, and wire; and (b) heating the mixtureat a temperature in the range of about 75° C. to about 250° C. to induceepitaxial layer-by-layer deposition of one or more zero-valent platinumoverlayers conformally deposited on the palladium nano-substrates, toproduce between one and ten platinum atomic overlayers.
 8. The fuel cellof claim 1, wherein the core-shell nanostructure is incorporated into anelectrode of the fuel cell.
 9. The fuel cell of claim 1, wherein thecore-shell nanostructure is an electrocatalyst for hydrogen oxidationreaction.
 10. The fuel cell of claim 9, wherein the core-shellnanostructure is incorporated at an anode of the fuel cell.
 11. The fuelcell of claim 1, wherein the core-shell nanostructure is anelectrocatalyst for oxygen reduction reaction.
 12. The fuel cell ofclaim 11, wherein the core-shell nanostructure is incorporated at acathode of the fuel cell.
 13. The fuel cell of claim 1, wherein thecore-shell nanostructure is incorporated in an electrically conductivesupport.
 14. The fuel cell of claim 13, wherein the electricallyconductive support comprises carbon, graphite, carbon nanotubes, carbonnanofibers, mesoporous carbon, graphene, acetylene black, or Ketjenblack.
 15. The fuel cell of claim 1, wherein the core-shellnanostructure has an electrochemically active surface area of at least10 m² per gram of platinum in the core-shell nanostructure.
 16. The fuelcell of claim 1, wherein the core-shell nanostructure has anelectrochemically active surface area of 15 m² per gram of platinum to125 m² per gram of platinum in the core-shell nanostructure.
 17. Thefuel cell of claim 1, wherein the core-shell nanostructure has a massactivity in the amount of 0.1 A per mg of platinum to 1.0 A per mg ofplatinum.
 18. The fuel cell of claim 1, wherein the fuel cell comprisesa proton exchange membrane fuel cell.
 19. A core-shell nanostructurecomprising a palladium nano-substrate conformally coated with betweenone and ten continuous uniform and smooth overlayers of epitaxiallydeposited zero-valent platinum atoms over the whole surface of thepalladium nano-substrate, the method comprising the steps of: (a)combining a first solution comprising a plurality of palladiumnano-substrates and a reducing agent with a second solution comprising aplatinum-containing compound to form a mixture, wherein the palladiumnano-substrate has a shape selected from the group consisting of cubic,concave cubic, tetrahedral, bipyramidal, octahedral, icosahedral,decahedral, rod, bar, and wire; and (b) heating the mixture at atemperature in the range of about 75° C. to about 250° C. to induceepitaxial layer-by-layer deposition of one or more zero-valent platinumoverlayers conformally deposited on the palladium nano-substrates, toproduce between one and ten platinum atomic overlayers.